Polymerization

Polymerization is a chemical process in which small molecules combine to form larger molecules that contain repeating structural units of the original molecules.

Typically, in a solvent, monomer molecules combine together in the presence of an initiator together in a chemical reaction to form polymer chains or 3D networks. Polymerization involves many reaction steps such as initiation, propagation, branching, termination. Many radicals of different chain lengths are formed. The final product is a mixture containing polymer molecules of varying lengths and structure.

This feature is based on the Method of Moments Model for polymerization. Primary properties like chain length distribution of polymer molecules are obtained by classical method of moments.

Simcenter STAR-CCM+ solves for the scalar transport of three Live polymers, λ 0 , λ 1 , and λ 2 , and three Dead polymers, μ 0 , μ 1 , and μ 2 . In addition to the source terms described below, Simcenter STAR-CCM+ allows you to add moment sources that you define. Simcenter STAR-CCM+ also solves for the scalar transport of the Initiator, Monomer, Radical, Solvent, and Modifier.

The source terms of the moment transport equations depend on the sub processes of polymerization:

  • Initiator Decomposition
    Figure 1. EQUATION_DISPLAY
    Iikdi2R,i=1,2,...,Ni
    (3781)
  • Chain Initiation
    Figure 2. EQUATION_DISPLAY
    R.+MkIR1
    (3782)

    where,

    the initiator consumption rate is found using:

    Figure 3. EQUATION_DISPLAY
    rIi=-kdi[Ii],i=1
    (3783)

    and the primary radical formation rate is found using:

    Figure 4. EQUATION_DISPLAY
    rR.=i=1Nd2fikdi[Ii]-kI[R.][M]
    (3784)

    where,

    f i = initiator efficiency

  • Propagation
    Figure 5. EQUATION_DISPLAY
    Rx+MkpRx+1
    (3785)

    where the monomer consumption rate is found using:

    Figure 6. EQUATION_DISPLAY
    rM=-kp[M]λ0
    (3786)
  • Chain transfer to monomer
    Figure 7. EQUATION_DISPLAY
    Rx+MktmPx+R1
    (3787)
  • Chain transfer to solvent
    Figure 8. EQUATION_DISPLAY
    Rx+SktsPx+R1
    (3788)

    where the solvent consumption rate is found using:

    Figure 9. EQUATION_DISPLAY
    rS=-kts[S]λ0
    (3789)
  • Chain transfer to polymer
    Figure 10. EQUATION_DISPLAY
    Rx+PyktsRy+Px
    (3790)
  • β -Scission
    Figure 11. EQUATION_DISPLAY
    Rx+PykβPx+Rz+Py-z=
    (3791)
  • Reaction with terminal double bond
    Figure 12. EQUATION_DISPLAY
    Rx+Py=kdbRx+y
    (3792)
  • Termination by disproportionation
    Figure 13. EQUATION_DISPLAY
    Rx+RyktdPx+Py
    (3793)
  • Termination by combination
    Figure 14. EQUATION_DISPLAY
    Rx+RyktcPx+y.
    (3794)

Simcenter STAR-CCM+ solves scalar transport equations for moments as follows:

  • For Live Polymers

    λ 0 is solved using r λ 0 as the source term

    Figure 15. EQUATION_DISPLAY
    λ0=n=1Rn
    (3795)

    where r λ 0 is defined by:

Figure 16. EQUATION_DISPLAY
rλ0=i=1Nd2fkdi[Ii]-(ktc+ktd)λ20
(3796)

λ 1 is solved using r λ 1 as the source term

Figure 17. EQUATION_DISPLAY
λ1=n=1nRn
(3797)

where r λ 1 is defined by:

Figure 18. EQUATION_DISPLAY
rλ1=i=1Nd2fkdi[Ii]-(ktm[M]+kts[S])λ1+kp[M]λ0-(ktc+ktd)λ0λ1+ktp(λ0μ2-λ1μ1)+kdbλ0μ1+kβ(12λ0μ2-λ1μ1)
(3798)

λ 2 is solved using r λ 2 as the source term

Figure 19. EQUATION_DISPLAY
λ2=n=1n2Rn
(3799)

where r λ 2 is defined by:

Figure 20. EQUATION_DISPLAY
rλ2=i=1Nd2fkdi[Ii]-(ktm[M]+kts[S])λ2+2kp[M]λ1-(ktc+ktd)λ0λ2+ktp(λ0μ3-λ2μ1)+kdb(2λ1μ1+λ0μ2)+kβ(13λ0μ3-12λ0μ2+16λ0μ1-λ2μ1)
(3800)
  • For Dead Polymers

    μ 0 is solved using r μ 0 as the source term

    Figure 21. EQUATION_DISPLAY
    μ0=n=1Pn
    (3801)

    where r μ 0 is defined by:

    Figure 22. EQUATION_DISPLAY
    rμ0=(ktm[M]+kts[S])λ0+(12ktc+ktd)λ20-kdbλ0μ0+kβλ0μ1
    (3802)

μ 1 is solved using r μ 1 as the source term

Figure 23. EQUATION_DISPLAY
μ1=n=1nPn
(3803)

where r μ 1 is defined by:

Figure 24. EQUATION_DISPLAY
rμ1=(ktm[M]+kts[S])λ1+(ktc+ktd)λ0λ1-ktp(λ0μ2-λ1μ1)-kdbλ0μ1+kβ(λ1μ1-12λ0μ2)
(3804)

μ 2 is solved using r μ 2 as the source term

Figure 25. EQUATION_DISPLAY
μ2=n=1n2Pn
(3805)

where r μ 2 is defined by:

Figure 26. EQUATION_DISPLAY
rμ2=(ktm[M]+kts[S])λ2+(ktc+ktd)λ0λ2+ktcλ21-ktp(λ0μ3-λ2μ1)-kdbλ0μ2+kβ[λ2μ1-λ0(23μ3+12μ2-16μ1)]
(3806)

The closure of the higher moment, μ 3 , is adopted from Pladis and Kiparissides [779].

In addition to the source terms and their jacobians for polymer scalars and polymer moments that are mentioned above, you can also include user-defined rates and jacobians for polymer scalar and moments sources.

Based on the specified Heat of Propagation and Heat of Initiation, appropriate source terms are added to the energy equation.

By solving the transport of the above six Moment equations, you can obtain information about the polymer molecular structure, such as Polydispersity and the Molecular Weight Distribution of the polymer. Simcenter STAR-CCM+ provides post-processing field functions for Polydispersity Index, Polymer Number-Averaged, and Mass-Averaged Chain Lengths. All Live and Dead Moments are also available as post-processing field functions.

Polydispersity Index is given by:

Figure 27. EQUATION_DISPLAY
μ 2 μ 0 μ 2 1
(3807)

Polymer Number-Averaged Chain Length (NACL) is given by:

Figure 28. EQUATION_DISPLAY
μ 1 μ 0
(3808)

Polymer Mass-Averaged Chain Length (MACL) is given by:

Figure 29. EQUATION_DISPLAY
μ 2 μ 1
(3809)